Techno-economic feasibility and life cycle assessment of dairy effluent to renewable diesel via hydrothermal liquefaction. (November 2015)

• Record Type: Journal Article
• Authors: Summers, Hailey M.; Ledbetter, Rhesa N.; McCurdy, Alex T.; Morgan, Michael R.; Seefeldt, Lance C.; Jena, Umakanta; Kent Hoekman, S.; Quinn, Jason C.
• Is Part Of: Bioresource technology. Volume 196(2015)
• Page Start: 431
• Page End: 440
• Publication Date: 2015-11
• Subjects: Net energy ratio -- Greenhouse gas emissions -- Techno-economic assessment -- Oleaginous yeast -- Cryptococcus curvatus; Biomass -- Periodicals; Biomass energy -- Periodicals; Bioremediation -- Periodicals; Agricultural wastes -- Periodicals; Factory and trade waste -- Periodicals; Organic wastes -- Periodicals; Bioénergie -- Périodiques; Déchets agricoles -- Périodiques; Déchets industriels -- Périodiques; Déchets organiques -- Périodiques; Déchets (Combustible) -- Périodiques; 662.88
• DOI: 10.1016/j.biortech.2015.07.077
• Languages: English
• ISSNs: 0960-8524

Abstract

Graphical abstract: Highlights: Demonstration of oleaginous yeast cultivated on delac to biocrude through HTL. Techno-economic modeling results in a fuel selling price of $4.78 per gallon. Life cycle results show a GHG emissions of 30 g-CO2 -eq MJ −1 and a NER of 0.81. Sensitivity analysis and optimization of production highlight areas for research. Abstract: The economic feasibility and environmental impact is investigated for the conversion of agricultural waste, delactosed whey permeate, through yeast fermentation to a renewable diesel via hydrothermal liquefaction. Process feasibility was demonstrated at laboratory-scale with data leveraged to validate systems models used to perform industrial-scale economic and environmental impact analyses. Results show a minimum fuel selling price of $4.78 per gallon of renewable diesel, a net energy ratio of 0.81, and greenhouse gas emissions of 30.0 g-CO2 -eq MJ −1 . High production costs and greenhouse gas emissions can be attributed to operational temperatures and durations of both fermentation and hydrothermal liquefaction. However, high lipid yields of the yeast counter these operational demands, resulting in a favorable net energy ratio. Results are presented on the optimization of the process based on economy of scale and a sensitivity analysis highlights improvements in conversion efficiency, yeast biomass productivity and hydrotreating efficiency can dramatically improve commercial feasibility.